US1314204A - Russell william mumford - Google Patents
Russell william mumford Download PDFInfo
- Publication number
- US1314204A US1314204A US1314204DA US1314204A US 1314204 A US1314204 A US 1314204A US 1314204D A US1314204D A US 1314204DA US 1314204 A US1314204 A US 1314204A
- Authority
- US
- United States
- Prior art keywords
- kieselguhr
- carbon
- charring
- decolorizing
- tar
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 30
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 19
- 229910052799 carbon Inorganic materials 0.000 description 19
- 239000000463 material Substances 0.000 description 15
- 238000000034 method Methods 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 238000002360 preparation method Methods 0.000 description 6
- 239000012629 purifying agent Substances 0.000 description 6
- 239000011269 tar Substances 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 5
- 239000011286 gas tar Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 230000001174 ascending effect Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000003077 lignite Substances 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 235000010755 mineral Nutrition 0.000 description 3
- 235000013311 vegetables Nutrition 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- 238000010000 carbonizing Methods 0.000 description 2
- 239000008395 clarifying agent Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000003415 peat Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 235000012712 vegetable carbon Nutrition 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000003712 decolorant Substances 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000010458 rotten stone Substances 0.000 description 1
- -1 sawdust Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 239000004108 vegetable carbon Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000011276 wood tar Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/14—Diatomaceous earth
Definitions
- This invention relates to processes of making purifying preparations; and it comprises a method of making a granular or powdery decolorant having also the ower of clarifying liquids and comprising I 'eselguhr containing incorporated therein a small amount of highly active decolorizing material and in admixture with a further amount of fine grained decolorizing carbon wherein kieselguhr is impregnated with ammoniacal tar or an equivalent material and, usually, is admixed with a further amount of material such as peat or brown coal capable of yieldin decolorizing carbon, and is then charred t rough a slowly ascending temperature range endin above 600 0.; all as more fully hereina er set forth and as claimed.
- Kieselguhr is often used. Kieselguhr or diatomaceous earth (tripoli) is com-posed of highly cellular microscopic silicious skeletons of micro-organism. It has little or no decolorizing power but has the power of clarifying liquids by attracting to itself suspended matters; a property connected in some way with its microscopic structure. Kieselguhr is often used for clarifying turbid liquids for this reason and is often used as an aftertreatment after decolorizing with vegetable carbons.
- Material so made is usually treated after completing the charring in such manner as to remove the mineral spacing agent.
- This dough of brown coal and tar-impregnated kieselguhr is formed into pellets or lumps and charred 1n a 0 Vented retort in the manner previously described; that is, heated so as to produce a slowly ascending temperature ending finally somewhere above 600 C.
- any usual type of furnace or retort may be 5 employed. It is often useful to blow through the retort a current of steam to re move va ors.
- the compound material After the compound material is made in the manner described, it is quickly cooled 5 to prevent spontaneous combustion". It may be dumped into water. I usually wash it and then dry. In drying in a rotary tube, the waste gases from the charring rnace or dry steam may be usefully employed.
- the excess of lime may be removed nally by treatment with acid or sedimentation.
- ammoniacal gas tar In lieu of using ammoniacal gas tar, I may use other tarry materials, such as asphalt, wood tar, etc., but I find the use of the ammoniacal gas tar more advantageous, since it leaves a residue of nitrogenous carbon (that is carbon containing nitrogen in combined form) which has very active decolorizing powers.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
UNITED STATES PATENT OFFICE.
RUSSELL WILLIAM MUMFORD, OF NEW YORK, N. Y., ASSIGNOR TO REFINING PRODUCTS CORPORATION, OF WILMINGTON, DELAWARE, A. CORPORATION OF DELAWARE.
PROCESS OF MAKING PURIFYING' PREPARATIONS.
1,314,204. No brewing.
To all whom it may concern:
Be it known that I Russnm. WILLIAM MUMFQRD, a citizen of the United States, residing at New York, in the county of New York and State of New York, have invented certain new and useful Improvements in Processes of Making Purifying Preparations, of which the following is a specification.
This invention relates to processes of making purifying preparations; and it comprises a method of making a granular or powdery decolorant having also the ower of clarifying liquids and comprising I 'eselguhr containing incorporated therein a small amount of highly active decolorizing material and in admixture with a further amount of fine grained decolorizing carbon wherein kieselguhr is impregnated with ammoniacal tar or an equivalent material and, usually, is admixed with a further amount of material such as peat or brown coal capable of yieldin decolorizing carbon, and is then charred t rough a slowly ascending temperature range endin above 600 0.; all as more fully hereina er set forth and as claimed.
In the purification of liquids for technical purposes, as in treating cane juice, molasses, syrup, glycerin, oil, etc., there are two types of purification usually desired. It is desirable to remove dissolved coloring matters and other impurities which, though not colored, are detrimental to the quality of the material; and it is also desirable to remove turbidity caused by finely divided matters in a state of suspension or semisolution; what are called colloidal suspensions. The purified liquid should not only be light colored, but absolutely clear or bright. In practice, two types of material are often used in succession. For the decolorizing, very finely divided carbons made from vegetable sources are in use. These preparations have a high adsorbing power and are active in removing coloring cause of the fineness of the carbons,
matter and other dissolved substances from the solutions. In order to heighten this power, which is one depending on surface action, it is the custom to make these powders very fine. They have no action, or very little, on suspended matters, or matters in a state of quasi-solution, and do not usually give bright or clear liquids. In fact, be-
they
Specification of Letters Patent.
Patented Aug. 26, 1919.
Application filed March 27. 1918. Serial 225.067.
often contribute turbidity, giving a blackish cloud to the solution. In order to remove this turbidity in the solution, it is often the practice to follow the treatment with the carbon by a treatment with a clarifying agent. For this purpose kieselguhr'is often used. Kieselguhr or diatomaceous earth (tripoli) is com-posed of highly cellular microscopic silicious skeletons of micro-organism. It has little or no decolorizing power but has the power of clarifying liquids by attracting to itself suspended matters; a property connected in some way with its microscopic structure. Kieselguhr is often used for clarifying turbid liquids for this reason and is often used as an aftertreatment after decolorizing with vegetable carbons.
It is the object of the present invention to make a composite preparation able to effect both decolorization and clarification; and to this end I treat kieselguhr so as to incorporate within its structure a certain amount of very porous decolorizing carbon. Kieselguhr is able to take up a certain amount of porous carbon without forfeiting the porosity of its own to which it owes its clarifying action and if the carbon so incorporated be produced in a proper manner, it will have a high decolorizing power. Further, the preparation may contain in addition to the carbon-impregnated kieselguhr particles, a certain amount of decolorizing carbon in mechanical admixture.
In another application, Serial No. 167 ,97 l, I have described and claimed a process of making decolorizin carbon having also a clarifying action w erein vegetable matters of various kinds are heated in a vented retort through a slowly ascending range of temperature ending above 600 C. In so heating the material, the gases and vapors which are evolved in the first charring action are given opportunity to escape from the char prior to themselves decomposing under the influence of heat with deposition of carbon. In order to secure an effective decolorizing carbon of not too fine a structure, it is necessary that it shall possess open pores representing as nearly as may be the or ginal structure of the material from which it was made; and that these pores shall not be clogged and obstructed by what may be called secondary carbon resulting from the charring in the pores of evolved'gases and vapors. In the stated application, in order to secure still more positively this effect, I have described the incorporation into the material prior to charring of a mineral spacing agent, such as finely ground dolomlte, etc., which has, together with several other functions that of spacing away the charring particles from each other and thereby faclhtatlng the removal of vapors, tar,
etc. Material so made is usually treated after completing the charring in such manner as to remove the mineral spacing agent.
I have found that I may use kieselguhr as the mineral spacing agent in securing this effect and 1n so doing I do not remove the kieselguhr afterward, since by letting it rernaln a compound decolorizing and clarifying agent of great efliciency may be procured. Indeed so desirableis the kieselguhr in this relation, that I may merely treat it in such a manner as to impregnate it with decolorizlng carbon without producing partl ClGS of decolorizing carbon between the kieselguhr particles.
In one embodiment of the present inventIon, making a material rich in kieselguhr and designed to have the clarifying funct1on 1n high degree, I do not mix any vegetable particles, such as sawdust, peat or brown coalwith the kieselguhr, but simply work the kieselguhr into a dough with wet gas tar. Ih1s gas tar should be material still containing ammonia. Or I may advantageously use gas liquor containing ammoma and more or less suspended or dissolved tar. On incorporatin tar or gas liquor with the kieselguhr, t e tar enters the pores, 1f not during the first incorporat1on, then during the first stages of'heating,
40 and on charring the kieselguhr in the descr bed manner I produceafa preparation w h1ch is virtually a carbon-impregnated kleselguhr; that is, all the granules of the material are kieselguhr granules and all the decolorizing carbon present is within these kieselguhr granules. In so doing, it is desirable to limit the amount of carbon, since the pores of the kieselguhr must not be too much clogged; they should be, so far as possible,'merely. lined with carbon.
In another embodiment, I work the kieselguhr into a dough with tar or the like as above and then mix with this dough a certain amount, say an equal amount, of brown 5 coal or lignite rich in volatile matters; this coal being in a finely powdered state, say, 80m 150 mesh. This dough of brown coal and tar-impregnated kieselguhr is formed into pellets or lumps and charred 1n a 0 Vented retort in the manner previously described; that is, heated so as to produce a slowly ascending temperature ending finally somewhere above 600 C. In the e g any usual type of furnace or retort may be 5 employed. It is often useful to blow through the retort a current of steam to re move va ors. Instead of using a retort it is a use ul expedient to place the material to be charred in thin layers in shallow iron pans and advance these charged pans, which may be covered, through a tunnellike furnace heated by surface combustion burners. Surface combustion as it is now understood, is the type of combustion produced by mixing air and gas in the theoretical proportions and allowing them to burn in the surface of a porous refractory block or pile of granules. In so doing, there being no excess oxygen, the products of combustion have little or no oxidizing 0 power on the carbon at the temperatures here contemplated and do not waste it away and do not interfere with its production.
After the compound material is made in the manner described, it is quickly cooled 5 to prevent spontaneous combustion". It may be dumped into water. I usually wash it and then dry. In drying in a rotary tube, the waste gases from the charring rnace or dry steam may be usefully employed.
In many embodiments of the present invention, I mix kieselguhr and carbonaceous material with a little milk of lime or a mixture of milk of lime and soluble phos hate. The excess of lime may be removed nally by treatment with acid or sedimentation.
In lieu of using ammoniacal gas tar, I may use other tarry materials, such as asphalt, wood tar, etc., but I find the use of the ammoniacal gas tar more advantageous, since it leaves a residue of nitrogenous carbon (that is carbon containing nitrogen in combined form) which has very active decolorizing powers.
What I claim is:
1. In the manufacture of purifying agents, the process which comprises impregnating kieselguhr with carbonaceous matter and slowly charrin through a range of temperatures ending a ove 600 0., the circumstances of charrin being such as to facilitate ready escape of vapors produced in the charring.
2. In the manufacture of purifying agents, the process which comprises impregnating kieselguhr with tarry matter and slowly charring through a range of temperature ending above 600 (1, the circumstances of charring being such as to I facilitate ready escape of vapors produced in charring.
3. In the manufacture of purifying agents, the process which comprises impregnating kieselguhr with ammoniacal gas tar and slowly charring through a range of vtemperature ending above 600 0., the circumstances of charring being such as to facilitate ready escape of vapors produced in charring.
4. In the manufacture of purifying agents,- the process which comprises impregnating kieselguhr with gas liquor containing ammonia and sus ended dissolved tarry matter and slowly c arrin the mixture in a vented retort throug -which a draft current of dry steam is passed to facilitate removal of vapors, and continuing the heating through a range of temperatures ending above 600 C.
5. In the manufacture of purifying agents, the process which comprises working kieselguhr and powdered carbonaceous matter together into a dough with a tarry 'matter and slowly carbonizing through a range of temperatures ending above 600 (3.,
the circumstances of charring being such as to facilitate ready'escape of vapors produced in charring. Y
6. In the manufacture of purifying agents, the process which comprises working kieselguhr and powdered vegetable carbon together into a dough with ammoniacal tarry matter and slowly carbonizing through a range of temperatures ending above 600 0., the circumstances of charring being such as to facilitate ready escape of vapors produced in charring.
In testimony whereof, I afiix my signature hereto.
RUSSELL WILLIAM MUMFORD.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1314204A true US1314204A (en) | 1919-08-26 |
Family
ID=3381696
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US1314204D Expired - Lifetime US1314204A (en) | Russell william mumford |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1314204A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2449016A (en) * | 1943-12-11 | 1948-09-07 | Socony Vacuum Oil Co Inc | Activation of petroleum adsorbents |
| US20100167921A1 (en) * | 2006-09-06 | 2010-07-01 | World Minerals, Inc. | Process for Roasting Diatomaceous Earth Ore to Reduce Organic Content |
-
0
- US US1314204D patent/US1314204A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2449016A (en) * | 1943-12-11 | 1948-09-07 | Socony Vacuum Oil Co Inc | Activation of petroleum adsorbents |
| US20100167921A1 (en) * | 2006-09-06 | 2010-07-01 | World Minerals, Inc. | Process for Roasting Diatomaceous Earth Ore to Reduce Organic Content |
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